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Further observations on the mean velocity distribution in fully developed pipe flow

Published online by Cambridge University Press:  23 February 2004

B. J. McKEON
Affiliation:
Department of Mechanical and Aerospace Engineering, Princeton University, Princeton, NJ 08544-0710, USA
J. LI
Affiliation:
Department of Mechanical and Aerospace Engineering, Princeton University, Princeton, NJ 08544-0710, USA Permanent address: School of the Built Environment, Victoria University of Technology, PO Box 14428, MCMC, Melbourne, Australia.
W. JIANG
Affiliation:
Department of Mechanical and Aerospace Engineering, Princeton University, Princeton, NJ 08544-0710, USA Permanent address: CARDC, PO Box 211 Mianyang, Sichuan 621000, P. R. China.
J. F. MORRISON
Affiliation:
Department of Mechanical and Aerospace Engineering, Princeton University, Princeton, NJ 08544-0710, USA Permanent address: Department of Aeronautics, Imperial College, London SW7 2BY, UK.
A. J. SMITS
Affiliation:
Department of Mechanical and Aerospace Engineering, Princeton University, Princeton, NJ 08544-0710, USA

Abstract

The measurements by Zagarola & Smits (1998) of mean velocity profiles in fully developed turbulent pipe flow are repeated using a smaller Pitot probe to reduce the uncertainties due to velocity gradient corrections. A new static pressure correction (McKeon & Smits 2002) is used in analysing all data and leads to significant differences from the Zagarola & Smits conclusions. The results confirm the presence of a power-law region near the wall and, for Reynolds numbers greater than $230\,{\times}\,10^3$ ($R^+\,{>}\,5\,{\times}\,10^3$), a logarithmic region further out, but the limits of these regions and some of the constants differ from those reported by Zagarola & Smits. In particular, the log law is found for $600\,{<}\, y^+\,{<}\,0.12R^+$ (instead of $600\,{<}\,y^+\,{<}\,0.07R^+$), and the von Kármán constant $\kappa$, the additive constant $B$ for the log law using inner flow scaling, and the additive constant $B^*$ for the log law using outer scaling are found to be $0.421 \pm 0.002$, $5.60 \pm 0.08 $ and $1.20 \pm 0.10$, respectively, with 95% confidence level (compared with $0.436 \pm 0.002$, $6.15 \pm 0.08$, and $1.51 \pm 0.03$ found by Zagarola & Smits). The data also confirm that the pipe flow data for Re$_D\,{\le}\,13.6\,{\times}\,10^6$ (as a minimum) are not affected by surface roughness.

Type
Papers
Copyright
© 2004 Cambridge University Press

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